SE447369B - PROCEDURE FOR THE PREPARATION OF PHOSPHIDS OF ALUMINUM OR MAGNESIUM - Google Patents
PROCEDURE FOR THE PREPARATION OF PHOSPHIDS OF ALUMINUM OR MAGNESIUMInfo
- Publication number
- SE447369B SE447369B SE8007910A SE8007910A SE447369B SE 447369 B SE447369 B SE 447369B SE 8007910 A SE8007910 A SE 8007910A SE 8007910 A SE8007910 A SE 8007910A SE 447369 B SE447369 B SE 447369B
- Authority
- SE
- Sweden
- Prior art keywords
- reaction
- phosphorus
- metal
- magnesium
- aluminum
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/08—Other phosphides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/08—Other phosphides
- C01B25/081—Other phosphides of alkali metals, alkaline-earth metals or magnesium
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/08—Other phosphides
- C01B25/082—Other phosphides of boron, aluminium, gallium or indium
- C01B25/085—Other phosphides of boron, aluminium, gallium or indium of aluminium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Spinning Or Twisting Of Yarns (AREA)
Description
447 369 ligger i form av pulver eller korn och om den gula fosforn tillsättes långsamt i flytande form. Det är dessutom fördel- aktigt om reaktionsblandningen under omsättningen omröres meka- niskt. 447 369 is in the form of powder or barley and if the yellow phosphorus is added slowly in liquid form. It is also advantageous if the reaction mixture is stirred mechanically during the reaction.
Genom förfarandet enligt uppfinningen är det möjligt att fram- ställa fosfiderna av aluminium eller magnesium eller en bland- ning av dessa fosfider i stora mängder utan risk och med i det närmaste teoretiskt utbyte. Förfarandet är mycket miljövänligt eftersom knappast några biprodukter bildas. Dessutom innehål- ler de bildade metallfosfiderna inga nämnvärda mängder poly- fosfider. Detta inverkar vid en efterföljande användning av dessa metallfosfider i bekämpningsmedel mot skadedjur genom att vid hydrolys av dessa i huvudsak endast fosforväte bildas, som icke självantändes i luft, däremot knappast högre fosfider, såsom difosfan, som är självantändliga.By the process according to the invention it is possible to produce the phosphides from aluminum or magnesium or a mixture of these phosphides in large quantities without risk and with the closest theoretical yield. The process is very environmentally friendly as hardly any by-products are formed. In addition, the metal phosphides formed do not contain significant amounts of polyphosphides. This has an effect on the subsequent use of these metal phosphides in pesticides by hydrolyzing them to produce essentially only phosphorus hydrogen which is not self-igniting in air, but hardly higher phosphides, such as diphosphane, which are self-igniting.
De vid förfarandet enligt uppfinningen såsom katalysatorer använda elementen klor, brom, jod eller dessas väte-, ammonium-, svavel-, fosfor-, zink-, aluminium- eller magnesiumföreningar, såsom HCl, NH4Cl, SCl2, SOCl2, SO2Cl2, PCl3, PBI3, PJ3, PCl5, PZJ4, POCl3, ZnCl2, Znßrz, AlCl3, AlBr3, MgCl2, MgBr2 eller MgJ2, användas lämpligen i sådan mängd, att viktförhållandet mellan den metall, som skall omsättas, och katalysatorn ligger i huvudsak inom området från l0OO0:l till lOOOO:200.The elements chlorine, bromine, iodine or their hydrogen, ammonium, sulfur, phosphorus, zinc, aluminum or magnesium compounds used in the process according to the invention as catalysts, such as HCl, NH4Cl, SC12, SOCl2, SO2Cl2, PCl3, PBI3 , PJ3, PC15, PZJ4, POCl3, ZnCl2, Znßrz, AlCl3, AlBr3, MgCl2, MgBr2 or MgJ2, are suitably used in such an amount that the weight ratio of the metal to be reacted to the catalyst is substantially in the range to 10000: 200.
Enligt en särskilt föredragen utföringsform av förfarandet enligt uppfinningen blandas först den finpulveriserade eller kornformiga metallen intimt med katalysatorn. Blandningen värmes i en lämplig, tillslutbar reaktor i inertgasatmosfär, exempelvis under kväve, vid normaltryck till reaktionstempcra- turen mellan 300 och 6OOOC. När den önskade reaktionstempera- turen uppnåtts tillföras flytande gul fosfor med sådan hastig- het att det frigjorda reaktionsvärmet utan problem kan bort- föras och temperaturen hållas inom området mellan 300 och GOOOC.According to a particularly preferred embodiment of the process according to the invention, the finely powdered or granular metal is first mixed intimately with the catalyst. The mixture is heated in a suitable, sealable reactor in an inert gas atmosphere, for example under nitrogen, at normal pressure to the reaction temperature between 300 and 600 ° C. When the desired reaction temperature is reached, liquid yellow phosphorus is added at such a rate that the heat of reaction released is easily removed and the temperature is kept in the range between 300 and 100 ° C.
Under dessa betingelser kan omsättningen lätt behärskas och den använda metallen smälter icke. När den erforderliga mängden fosfor tillsatts upprütthålles lämpligen en oftcrreaktionstid 447 369 av lämplig varaktighet för att möjliggöra en i möjligaste mån fullständig omsättning. Även under efterreaktionstiden hålles temperaturen inom området mellan 300 och 60006. När omsätt- ningen avslutats uttages reaktionsprodukten under inertgas genom en under reaktorn anordnad utloppsanordning i varmt tillstånd.Under these conditions, the reaction can be easily controlled and the metal used does not melt. When the required amount of phosphorus has been added, an often reaction time of 447,369 of suitable duration is suitably maintained to enable as complete a conversion as possible. Even during the post-reaction time, the temperature is kept in the range between 300 and 60006. When the reaction is completed, the reaction product is taken out under inert gas through an outlet device arranged below the reactor in a hot state.
Uppfinningen beskrives närmare med följande utföringsexempel.The invention is described in more detail with the following working examples.
Exemgel l. 200 g magnesiumkorn upphettas under kväve med 0,8 g jod i ett med ett vattenföriag tiiisiutet reaktionskari till 35o°c.Example 1. 200 g of magnesium granules are heated under nitrogen with 0.8 g of iodine in a reaction vessel heated to 35 DEG C. with an aqueous solution.
Upphettningen avbrytes och 157 g gul fosfor inblanåas i reak- tionsblandningen i flytande form så långsamt att temperaturen icke stiger över SOOOC. Tillföringstiden är cirka 30 minuter.The heating is stopped and 157 g of yellow phosphorus are blended into the reaction mixture in liquid form so slowly that the temperature does not rise above 50 ° C. The delivery time is about 30 minutes.
Den gråa kornformiga produkten kan utan svårigheter uttagas ur reaktorn.The gray granular product can be removed from the reactor without difficulty.
Utbyte: 356 g; halt av Mg3P2: 89 %.Yield: 356 g; content of Mg3P2: 89%.
Exempel 2. 400 g magnesiumkorn upphettas i ett med ett vattenförlag till- slutet reaktionskärl under kväve vid mekanisk omröring till 300°C. I en dropptratt blandas 320 g gul fosfor och 3 g jod och värmes till 5O0C. Fosfor-jod-blandningen tillföres lång- samt till den upphettade metallen. Tillföringstid: cirka 25 minuter. Temperaturen stiger till 5lOOC. I Utbyte: 7l5 g; halt av Mg3P2: 94,5 %.Example 2. 400 g of magnesium granules are heated in a reaction vessel closed with a water source under nitrogen by mechanical stirring to 300 ° C. In a dropping funnel, 320 g of yellow phosphorus and 3 g of iodine are mixed and heated to 5 ° C. The phosphorus-iodine mixture is slowly added to the heated metal. Delivery time: about 25 minutes. The temperature rises to 51 ° C. In Yield: 715 g; content of Mg3P2: 94.5%.
Exemoel 3. 200 g magnesiumkorn blandas under kväve med l g difosfortetra- jodid i ett med ett vattenförlag tillslutet reaktionskärl och upphettas till 360°C. Sedan upphettningen avslutats tillföres l62 g flytande gul fosfor så långsamt, att temperaturen icke stiger över 5oO°C. Tillföringstid: cirka 25 minuter. Den gråa, kornformiga produkten kan utan svårigheter uttagas ur reaktorn.Exemoel 3. 200 g of magnesium granules are mixed under nitrogen with 1 g of diphosphorus tetraiodide in a reaction vessel closed with a water source and heated to 360 ° C. After the heating is completed, 162 g of liquid yellow phosphorus are added so slowly that the temperature does not rise above 50 ° C. Delivery time: about 25 minutes. The gray, granular product can be removed from the reactor without difficulty.
Utbyte: 361 g; halt av Mg3P2: 95,5 %. 447 369 âgemgel 4. l00 g magnesiumkorn blandas under kväve med 3 g brom i ett med ett vattenförlag tillslutet reaktionskärl och upphettas till 300OC. Sedan upphettningen avslutats tillföres långsamt v 80 g flytande gul fosfor till reaktionsblandningen.-Eempera- turen stiger icke över 480°C. Tillföringstid: cirka 35 minuter. ¿ Den gråa, kornformiga produkten kan utan svårigheter utskakas Q ur reaktorn.Yield: 361 g; content of Mg3P2: 95.5%. 447 369 âgemgel 4. 100 g of magnesium granules are mixed under nitrogen with 3 g of bromine in a reaction vessel closed with a water source and heated to 300 ° C. After the heating is completed, 80 g of liquid yellow phosphorus are slowly added to the reaction mixture. The temperature does not rise above 480 ° C. Delivery time: about 35 minutes. ¿The gray, granular product can be easily shaken out of the reactor.
Utbyte: 178 g; halt av Mg3P2: 89 %.Yield: 178 g; content of Mg3P2: 89%.
Exembel 5. g magnesiumkorn upphettas under kväve i ett med ett vatten- förlag tillslutet reaktionskärl till 320°C. Sedan upphettningen avbrutits tillföres långsamt en flytande blandning av 24 g gul fosfor och 0,3 g brom till reaktionskärlet. Temperaturen stiger icke över 390°C. Tillföringstid: 20 minuter. Reaktions- blandningen hålles ytterligare 20 minuter vid 380°C varefter den kornformiga produkten utan svårighet kan utskakas ur reak- torn. , Utbyte: 54 g; halt av Mg3P2: 87 %.Example 5. g of magnesium granules is heated under nitrogen in a reaction vessel closed with a water source to 320 ° C. After the heating is stopped, a liquid mixture of 24 g of yellow phosphorus and 0.3 g of bromine is slowly added to the reaction vessel. The temperature does not rise above 390 ° C. Delivery time: 20 minutes. The reaction mixture is kept for a further 20 minutes at 380 ° C, after which the granular product can be shaken out of the reactor without difficulty. Yield: 54 g; content of Mg3P2: 87%.
Exemgel 6. kg magnesiumkorn blandas med 40 g jod i ett med ett vatten- förlag tillslutet reaktionskärl och upphettas till 35006. Sedan upphettningen avbrutits tillföres långsamt 8,5 kg flytande gul fosfor till reaktionsblandningen. Under tillsatsen stiger tem- peraturen icke över 48000. Reaktionsblandningen omröres meka- niskt under hela reaktionstiden. Tillföringstid: 70 minuter.Example gel 6. kg of magnesium granules is mixed with 40 g of iodine in a reaction vessel closed with a water reservoir and heated to 35006. After the heating is stopped, 8.5 kg of liquid yellow phosphorus are slowly added to the reaction mixture. During the addition, the temperature does not rise above 48,000. The reaction mixture is stirred mechanically throughout the reaction time. Delivery time: 70 minutes.
Den gråa, kornformiga produkten uttages nedtill genom en öppning utan att reaktorn öppnas ytterligare.The gray, granular product is removed at the bottom through an opening without further opening the reactor.
Utbyte: 18,4 kg; halt av Mg3P2: 95 %.Yield: 18.4 kg; content of Mg3P2: 95%.
Exemgel 7. 100 g magnesium-aluminium-legering (50 % magnesium, 50 % alumi- nium) blandas i ett med ett vattenförlag tillslutet reaktions- kärl under kväve med 2 q brom och upphettes till 33o°c. sedan upphettningen avbrutits tillföres långsamt 100 g flytande gul fosfor till reaktionsblandningen. Temperaturen stiger icke över . 447 369 45OOC. Tillföringstid: cirka 30 minuter. Den gråa, kornformiga produkten kan utan svårigheter utskakas ur reaktorn.Example gel 7. 100 g of magnesium-aluminum alloy (50% magnesium, 50% aluminum) are mixed in a reaction vessel closed with a water source under nitrogen with 2 g of bromine and heated to 33 ° C. after the heating is stopped, 100 g of liquid yellow phosphorus are slowly added to the reaction mixture. The temperature does not rise above. 447 369 45OOC. Delivery time: about 30 minutes. The gray, granular product can be easily removed from the reactor.
Utbyte: 200 g; halt av magnesiumfosfid och aluminiumfosfid: 95 %. âxempel 8. l,5 kg magnesium-aluminium-legering (50 % magnesium, 50 % alu- minium) blandas under kväve med l5 g jod i ett med ett vatten- förlag tillslutet reaktionskärl och upphettas till 36OOC. Sedan upphettningen avbrutits tillföres långsamt 1,5 kg flytande gul fosfor till reaktionsblandningen. Temperaturen stiger icke över 450°C. Tillföringstid: 30 minuter. Den gråa, kornformiga produk- ten kan utan svårigheter utskakas ur reaktorn.Yield: 200 g; content of magnesium phosphide and aluminum phosphide: 95%. Example 8. 1.5 kg of magnesium-aluminum alloy (50% magnesium, 50% aluminum) are mixed under nitrogen with 15 g of iodine in a reaction vessel closed with a water source and heated to 36 DEG C. After the heating is stopped, 1.5 kg of liquid yellow phosphorus are slowly added to the reaction mixture. The temperature does not rise above 450 ° C. Delivery time: 30 minutes. The gray, granular product can be easily removed from the reactor.
Utbyte: 2,9 kg; halt av magnesiumfosfid och aluminiumfosfid: 90 %.Yield: 2.9 kg; content of magnesium phosphide and aluminum phosphide: 90%.
Exempel 9. 64 g aluminium-korn blandas under kväve med l g jod i ett med ett vattenförlag tillslutet reaktionskärl och upphettas till 38OOC. Sedan upphettningen avbrutits tillföres långsamt 62 g flytande gul fosfor. Temperaturen stiger härvid icke över SOOOC. Tillföringstid: cirka 30 minuter. Den gråa, kornformiga produkten kan utan svårigheter utskakas ur reaktorn.Example 9. 64 g of aluminum granules are mixed under nitrogen with 1 g of iodine in a reaction vessel closed with a water source and heated to 38 ° C. After the heating is stopped, 62 g of liquid yellow phosphorus are slowly added. The temperature does not rise above SOOOC. Delivery time: about 30 minutes. The gray, granular product can be easily removed from the reactor.
Q Utbyte: 122 g; halt av aluminiumfosfid: 85 a.Q Yield: 122 g; content of aluminum phosphide: 85 a.
Claims (6)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2945647A DE2945647C2 (en) | 1979-11-12 | 1979-11-12 | Process for the production of aluminum phosphide and / or magnesium phosphide |
Publications (2)
Publication Number | Publication Date |
---|---|
SE8007910L SE8007910L (en) | 1981-05-13 |
SE447369B true SE447369B (en) | 1986-11-10 |
Family
ID=6085785
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE8007910A SE447369B (en) | 1979-11-12 | 1980-11-11 | PROCEDURE FOR THE PREPARATION OF PHOSPHIDS OF ALUMINUM OR MAGNESIUM |
Country Status (18)
Country | Link |
---|---|
US (2) | US4331642A (en) |
JP (1) | JPS5684306A (en) |
AT (1) | AT392629B (en) |
AU (1) | AU532514B2 (en) |
BR (1) | BR8007320A (en) |
CA (1) | CA1124987A (en) |
DE (1) | DE2945647C2 (en) |
DK (1) | DK146820C (en) |
ES (1) | ES496319A0 (en) |
FI (1) | FI64930C (en) |
FR (2) | FR2470089A1 (en) |
GB (1) | GB2062602B (en) |
IE (1) | IE50371B1 (en) |
IT (1) | IT1129834B (en) |
MX (1) | MX154185A (en) |
NO (1) | NO151699C (en) |
SE (1) | SE447369B (en) |
ZA (1) | ZA806133B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2945647C2 (en) * | 1979-11-12 | 1990-01-04 | Degesch Gmbh, 6000 Frankfurt | Process for the production of aluminum phosphide and / or magnesium phosphide |
DE3117393A1 (en) * | 1981-05-02 | 1982-11-11 | Degesch Gmbh, 6000 Frankfurt | METHOD FOR PRODUCING THE PHOSPHIDES OF ALUMINUM OR MAGNESIUM |
GB9511495D0 (en) * | 1995-06-07 | 1995-08-02 | Degesch De Chile Ltda | Composition, process and apparatus for producing phosphine - containing gas |
US6047497A (en) | 1997-03-18 | 2000-04-11 | The Boc Group, Inc. | Gas fumigation method and system |
CN1107447C (en) * | 1999-04-27 | 2003-05-07 | 华仁沈阳农药有限公司 | Process for synthesizing magnesium phosphide as fumigating insecticide of storehouse |
CN102351158B (en) * | 2011-07-14 | 2013-02-13 | 马文忠 | Process of producing aluminum phosphide from yellow phosphorus and recovering byproducts simultaneously |
CA3029934A1 (en) * | 2016-07-04 | 2018-01-11 | Hokko Chemical Industry Co., Ltd. | Organic magnesium phosphide and manufacturing method thereof, organic magnesium phosphide complex and manufacturing method thereof, and manufacturing method of organic phosphorus compound using said phosphide |
AR115373A1 (en) * | 2018-04-27 | 2021-01-13 | Gasapps Australia Pty Ltd | GAS SUPPLY SYSTEM |
CN110950909B (en) * | 2018-09-27 | 2022-07-15 | 紫石能源有限公司 | Process for the preparation of trimethylphosphine |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE736700C (en) * | 1940-03-13 | 1943-06-28 | Schering Ag | Manufacture of products containing magnesium phosphide |
US3008805A (en) * | 1959-06-09 | 1961-11-14 | Gen Electric | Preparation of metal phosphides |
US3269103A (en) * | 1963-12-21 | 1966-08-30 | Palitex Project Co Gmbh | A device for arresting a multiple twist spindle |
CH515852A (en) * | 1966-04-07 | 1971-11-30 | Freyberg Werner Dr | Magnesium phosphide mg3p2 fumigating agent for cereals |
DE1567520B2 (en) * | 1966-04-07 | 1973-01-04 | Freyberg, Werner, Dr., 6149 Kirschhausen | Process for the production of magnesium phosphide |
DE1685942B1 (en) * | 1967-06-23 | 1971-07-15 | Palitex Project Co Gmbh | Stopping device for the rotor of a two-for-one twisting spindle |
US3899572A (en) * | 1969-12-13 | 1975-08-12 | Sony Corp | Process for producing phosphides |
DE2159075C3 (en) * | 1971-11-29 | 1975-01-02 | Palitex Project-Company Gmbh, 4150 Krefeld | Device for braking and stopping a two-for-one twisting spindle with tangential belt drive in a predetermined position |
DE2945647C2 (en) * | 1979-11-12 | 1990-01-04 | Degesch Gmbh, 6000 Frankfurt | Process for the production of aluminum phosphide and / or magnesium phosphide |
-
1979
- 1979-11-12 DE DE2945647A patent/DE2945647C2/en not_active Expired - Lifetime
-
1980
- 1980-09-30 FR FR8020966A patent/FR2470089A1/en active Granted
- 1980-09-30 FR FR8020906A patent/FR2469479A1/en active Pending
- 1980-10-03 ZA ZA00806133A patent/ZA806133B/en unknown
- 1980-10-03 US US06/193,481 patent/US4331642A/en not_active Expired - Lifetime
- 1980-10-21 AU AU63552/80A patent/AU532514B2/en not_active Expired
- 1980-10-22 NO NO803141A patent/NO151699C/en unknown
- 1980-10-23 JP JP14885780A patent/JPS5684306A/en active Granted
- 1980-10-28 ES ES496319A patent/ES496319A0/en active Granted
- 1980-11-06 GB GB8035748A patent/GB2062602B/en not_active Expired
- 1980-11-07 CA CA364,289A patent/CA1124987A/en not_active Expired
- 1980-11-07 DK DK474080A patent/DK146820C/en not_active IP Right Cessation
- 1980-11-11 BR BR8007320A patent/BR8007320A/en unknown
- 1980-11-11 IT IT68722/80A patent/IT1129834B/en active
- 1980-11-11 AT AT5542/80A patent/AT392629B/en not_active IP Right Cessation
- 1980-11-11 IE IE2330/80A patent/IE50371B1/en unknown
- 1980-11-11 MX MX184705A patent/MX154185A/en unknown
- 1980-11-11 SE SE8007910A patent/SE447369B/en not_active IP Right Cessation
- 1980-11-12 FI FI803537A patent/FI64930C/en not_active IP Right Cessation
-
1982
- 1982-04-05 US US06/365,322 patent/US4412979A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
NO803141L (en) | 1981-05-13 |
FR2470089B1 (en) | 1984-07-20 |
NO151699B (en) | 1985-02-11 |
ES8107122A1 (en) | 1981-10-01 |
AT392629B (en) | 1991-05-10 |
GB2062602B (en) | 1983-06-02 |
FR2469479A1 (en) | 1981-05-22 |
IT8068722A0 (en) | 1980-11-11 |
ES496319A0 (en) | 1981-10-01 |
DK474080A (en) | 1981-05-13 |
IE50371B1 (en) | 1986-04-02 |
US4331642A (en) | 1982-05-25 |
FI64930B (en) | 1983-10-31 |
US4412979A (en) | 1983-11-01 |
SE8007910L (en) | 1981-05-13 |
BR8007320A (en) | 1981-05-26 |
AU532514B2 (en) | 1983-10-06 |
IT1129834B (en) | 1986-06-11 |
GB2062602A (en) | 1981-05-28 |
AU6355280A (en) | 1981-05-21 |
ATA554280A (en) | 1990-10-15 |
IE802330L (en) | 1981-05-12 |
DE2945647C2 (en) | 1990-01-04 |
ZA806133B (en) | 1981-09-30 |
FR2470089A1 (en) | 1981-05-29 |
DK146820C (en) | 1984-06-25 |
DE2945647A1 (en) | 1981-05-21 |
FI803537L (en) | 1981-05-13 |
MX154185A (en) | 1987-06-03 |
CA1124987A (en) | 1982-06-08 |
JPS5684306A (en) | 1981-07-09 |
DK146820B (en) | 1984-01-16 |
FI64930C (en) | 1984-02-10 |
NO151699C (en) | 1985-05-22 |
JPS647006B2 (en) | 1989-02-07 |
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